Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems

Detalhes bibliográficos
Autor(a) principal: Panas, Paweł [UNESP]
Data de Publicação: 2017
Outros Autores: Lopes, Camila [UNESP], Cerri, Marcel O. [UNESP], Ventura, Sónia P.M., Santos-Ebinuma, Valéria C. [UNESP], Pereira, Jorge F.B. [UNESP]
Tipo de documento: Artigo
Idioma: eng
Título da fonte: Repositório Institucional da UNESP
Texto Completo: http://dx.doi.org/10.1016/j.fluid.2017.07.005
http://hdl.handle.net/11449/169959
Resumo: Clavulanic acid (CA) is an important pharmaceutical compound produced by batch fermentation of Streptomyces clavuligerus. Since, CA is chemically unstable, its downstream processing should be studied to develop more efficient and resolute techniques. Herein, the use of aqueous two-phase systems (ATPS) composed of cholinium chloride, [Ch]Cl, was proposed as a novel platform for the recovery and purification of CA. Thus, the stability of CA in presence of different [Ch]Cl concentrations was initially studied, and the high biocompatibility of this salt was demonstrated by the low CA degradation levels. Then, the partitioning of CA using two types of polymeric ATPS has been investigated. Two ATPS formed by the combination of [Ch]Cl and two polyethylene glycol (PEG) polymers, PEG 600 g mol−1 (PEG-600) and polyethylene glycol methyl ether 550 g mol−1 (PEG-500-OMe), were used to assess the influence of the PEG nature, in addition to the concentration of the phase forming agents on the CA partitioning. It has shown that CA is almost equally distributed between the two-phases in equilibrium (0.6 < KCA < 1.6). Nevertheless, the selective extraction of CA for the [Ch]Cl-rich or PEG-rich phase by the proper adjustment of ATPS composition was attained. In the search for higher extraction efficiencies [EE (%)] and partition coefficients (KCA), a second polymeric ATPS platform composed of PEG-600 and sodium polyacrylate 8000 g mol−1 (NaPA-8000), applying [Ch]Cl as adjuvant was tested. The main results suggest the recovery of CA towards the PEG-rich phase (KCA ≥ 5.6 ± 0.6 and EE ≥ 85.5± 1.4%). The higher migration levels of CA have mainly resulted from the electronegative repulsion of NaPA-8000 over CA molecules. The ATPS with best performance for the CA extraction were selected for the recovery of CA directly from fermented broth of Streptomyces clavuligerus. In this set of experiments, the highest values of CA recovery yield and purification factor (respectively, 64.91± 1.99% and 22.70 ± 0.87) were attained for the systems PEG-600/NaPA-8000 and PEG-600/[Ch]Cl, respectively.
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spelling Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systemsAqueous two-phase systemsCholinium chlorideClavulanic acidPolyethylene glycolStreptomyces clavuligerusClavulanic acid (CA) is an important pharmaceutical compound produced by batch fermentation of Streptomyces clavuligerus. Since, CA is chemically unstable, its downstream processing should be studied to develop more efficient and resolute techniques. Herein, the use of aqueous two-phase systems (ATPS) composed of cholinium chloride, [Ch]Cl, was proposed as a novel platform for the recovery and purification of CA. Thus, the stability of CA in presence of different [Ch]Cl concentrations was initially studied, and the high biocompatibility of this salt was demonstrated by the low CA degradation levels. Then, the partitioning of CA using two types of polymeric ATPS has been investigated. Two ATPS formed by the combination of [Ch]Cl and two polyethylene glycol (PEG) polymers, PEG 600 g mol−1 (PEG-600) and polyethylene glycol methyl ether 550 g mol−1 (PEG-500-OMe), were used to assess the influence of the PEG nature, in addition to the concentration of the phase forming agents on the CA partitioning. It has shown that CA is almost equally distributed between the two-phases in equilibrium (0.6 < KCA < 1.6). Nevertheless, the selective extraction of CA for the [Ch]Cl-rich or PEG-rich phase by the proper adjustment of ATPS composition was attained. In the search for higher extraction efficiencies [EE (%)] and partition coefficients (KCA), a second polymeric ATPS platform composed of PEG-600 and sodium polyacrylate 8000 g mol−1 (NaPA-8000), applying [Ch]Cl as adjuvant was tested. The main results suggest the recovery of CA towards the PEG-rich phase (KCA ≥ 5.6 ± 0.6 and EE ≥ 85.5± 1.4%). The higher migration levels of CA have mainly resulted from the electronegative repulsion of NaPA-8000 over CA molecules. The ATPS with best performance for the CA extraction were selected for the recovery of CA directly from fermented broth of Streptomyces clavuligerus. In this set of experiments, the highest values of CA recovery yield and purification factor (respectively, 64.91± 1.99% and 22.70 ± 0.87) were attained for the systems PEG-600/NaPA-8000 and PEG-600/[Ch]Cl, respectively.Coordenação de Aperfeiçoamento de Pessoal de Nível Superior (CAPES)Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Federación Española de Enfermedades RarasDepartment of Bioprocess and Biotechnology School of Pharmaceutical Sciences UNESP – Univ Estadual Paulista, Rodovia Araraquara-Jaú/01, Campos VilleInstitute of Botany Leibniz Universität Hannover, Herrenhäuser Str. 2CICECO – Aveiro Institute of Materials Department of Chemistry University of AveiroDepartment of Bioprocess and Biotechnology School of Pharmaceutical Sciences UNESP – Univ Estadual Paulista, Rodovia Araraquara-Jaú/01, Campos VilleFAPESP: 2014/01580-3Federación Española de Enfermedades Raras: PT2020Universidade Estadual Paulista (Unesp)Leibniz Universität HannoverUniversity of AveiroPanas, Paweł [UNESP]Lopes, Camila [UNESP]Cerri, Marcel O. [UNESP]Ventura, Sónia P.M.Santos-Ebinuma, Valéria C. [UNESP]Pereira, Jorge F.B. [UNESP]2018-12-11T16:48:26Z2018-12-11T16:48:26Z2017-10-25info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article42-50application/pdfhttp://dx.doi.org/10.1016/j.fluid.2017.07.005Fluid Phase Equilibria, v. 450, p. 42-50.0378-3812http://hdl.handle.net/11449/16995910.1016/j.fluid.2017.07.0052-s2.0-850256287782-s2.0-85025628778.pdfScopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengFluid Phase Equilibria0,950info:eu-repo/semantics/openAccess2024-01-03T06:21:15Zoai:repositorio.unesp.br:11449/169959Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T22:00:08.131065Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false
dc.title.none.fl_str_mv Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems
title Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems
spellingShingle Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems
Panas, Paweł [UNESP]
Aqueous two-phase systems
Cholinium chloride
Clavulanic acid
Polyethylene glycol
Streptomyces clavuligerus
title_short Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems
title_full Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems
title_fullStr Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems
title_full_unstemmed Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems
title_sort Purification of clavulanic acid produced by Streptomyces clavuligerus via submerged fermentation using polyethylene glycol/cholinium chloride aqueous two-phase systems
author Panas, Paweł [UNESP]
author_facet Panas, Paweł [UNESP]
Lopes, Camila [UNESP]
Cerri, Marcel O. [UNESP]
Ventura, Sónia P.M.
Santos-Ebinuma, Valéria C. [UNESP]
Pereira, Jorge F.B. [UNESP]
author_role author
author2 Lopes, Camila [UNESP]
Cerri, Marcel O. [UNESP]
Ventura, Sónia P.M.
Santos-Ebinuma, Valéria C. [UNESP]
Pereira, Jorge F.B. [UNESP]
author2_role author
author
author
author
author
dc.contributor.none.fl_str_mv Universidade Estadual Paulista (Unesp)
Leibniz Universität Hannover
University of Aveiro
dc.contributor.author.fl_str_mv Panas, Paweł [UNESP]
Lopes, Camila [UNESP]
Cerri, Marcel O. [UNESP]
Ventura, Sónia P.M.
Santos-Ebinuma, Valéria C. [UNESP]
Pereira, Jorge F.B. [UNESP]
dc.subject.por.fl_str_mv Aqueous two-phase systems
Cholinium chloride
Clavulanic acid
Polyethylene glycol
Streptomyces clavuligerus
topic Aqueous two-phase systems
Cholinium chloride
Clavulanic acid
Polyethylene glycol
Streptomyces clavuligerus
description Clavulanic acid (CA) is an important pharmaceutical compound produced by batch fermentation of Streptomyces clavuligerus. Since, CA is chemically unstable, its downstream processing should be studied to develop more efficient and resolute techniques. Herein, the use of aqueous two-phase systems (ATPS) composed of cholinium chloride, [Ch]Cl, was proposed as a novel platform for the recovery and purification of CA. Thus, the stability of CA in presence of different [Ch]Cl concentrations was initially studied, and the high biocompatibility of this salt was demonstrated by the low CA degradation levels. Then, the partitioning of CA using two types of polymeric ATPS has been investigated. Two ATPS formed by the combination of [Ch]Cl and two polyethylene glycol (PEG) polymers, PEG 600 g mol−1 (PEG-600) and polyethylene glycol methyl ether 550 g mol−1 (PEG-500-OMe), were used to assess the influence of the PEG nature, in addition to the concentration of the phase forming agents on the CA partitioning. It has shown that CA is almost equally distributed between the two-phases in equilibrium (0.6 < KCA < 1.6). Nevertheless, the selective extraction of CA for the [Ch]Cl-rich or PEG-rich phase by the proper adjustment of ATPS composition was attained. In the search for higher extraction efficiencies [EE (%)] and partition coefficients (KCA), a second polymeric ATPS platform composed of PEG-600 and sodium polyacrylate 8000 g mol−1 (NaPA-8000), applying [Ch]Cl as adjuvant was tested. The main results suggest the recovery of CA towards the PEG-rich phase (KCA ≥ 5.6 ± 0.6 and EE ≥ 85.5± 1.4%). The higher migration levels of CA have mainly resulted from the electronegative repulsion of NaPA-8000 over CA molecules. The ATPS with best performance for the CA extraction were selected for the recovery of CA directly from fermented broth of Streptomyces clavuligerus. In this set of experiments, the highest values of CA recovery yield and purification factor (respectively, 64.91± 1.99% and 22.70 ± 0.87) were attained for the systems PEG-600/NaPA-8000 and PEG-600/[Ch]Cl, respectively.
publishDate 2017
dc.date.none.fl_str_mv 2017-10-25
2018-12-11T16:48:26Z
2018-12-11T16:48:26Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
format article
status_str publishedVersion
dc.identifier.uri.fl_str_mv http://dx.doi.org/10.1016/j.fluid.2017.07.005
Fluid Phase Equilibria, v. 450, p. 42-50.
0378-3812
http://hdl.handle.net/11449/169959
10.1016/j.fluid.2017.07.005
2-s2.0-85025628778
2-s2.0-85025628778.pdf
url http://dx.doi.org/10.1016/j.fluid.2017.07.005
http://hdl.handle.net/11449/169959
identifier_str_mv Fluid Phase Equilibria, v. 450, p. 42-50.
0378-3812
10.1016/j.fluid.2017.07.005
2-s2.0-85025628778
2-s2.0-85025628778.pdf
dc.language.iso.fl_str_mv eng
language eng
dc.relation.none.fl_str_mv Fluid Phase Equilibria
0,950
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv 42-50
application/pdf
dc.source.none.fl_str_mv Scopus
reponame:Repositório Institucional da UNESP
instname:Universidade Estadual Paulista (UNESP)
instacron:UNESP
instname_str Universidade Estadual Paulista (UNESP)
instacron_str UNESP
institution UNESP
reponame_str Repositório Institucional da UNESP
collection Repositório Institucional da UNESP
repository.name.fl_str_mv Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)
repository.mail.fl_str_mv
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